Screw extruder and gear pump arrangement for highly viscous media

ABSTRACT

The invention relates to a screw extruder and gear pump arrangement for highly viscous media, in particular for plastic melts and rubber mixtures, having one or more screw shafts and a gear pump which, in drive terms, is coupled mechanically to the screw shaft or shafts and whose pump casing is a constituent part of the casing of the screw extruder or is connected directly thereto.

[0001] The invention relates to a screw extruder and gear pump arrangement for highly viscous media.

[0002] DE-A 21 00 403 discloses a hydraulic pump which, in the form of an epicyclic gearbox, is equipped with a sun gear, a plurality of planet gears rotatably mounted on a planet carrier and an internal gear, all the gears having teeth. Between the planet gears and the internal gear, which intermesh, and also between the planet gears and the sun gear, which likewise intermesh, suction and pressure chamber elements are formed alternately, being sealed off by arcuate dividing walls of the planet carrier, which otherwise fills the interspaces between the gears. The flat sides of the planet gears, of the internal gear and of the sun gear in each case bear in a leakproof manner on two flat casing walls arranged at a distance from each other, which are provided with wall apertures which connect the individual suction and pressure chamber elements between the gears with a suction chamber provided with a hydraulic feed line and functioning as a collector and, respectively, with a pressure chamber provided with a hydraulic line and likewise functioning as a collector. In the case of this known gear pump, which has to be designated a planet gear pump, the planet carrier is preferably fixed, while the sun gear and the internal gear revolve. Such a pump is basically less suitable for delivering highly viscous media, since it would have to be fed with a considerable pilot pressure and thus would not be self cleaning.

[0003] A similar gear pump, which is disclosed by DE 36 31 527 C1, permits its delivery rate to be varied independently of speed. The pump again has toothed planet gears, a planet carrier and a toothed internal gear and also a toothed sun gear, which are enclosed on the outside by a pump casing. In order to change the delivery rate, independently of the speed of the driven sun gear, optionally the revolving movement of the planet carrier or the rotational movement of the internal gear can be stopped. The planet carrier is provided with an inlet sealing wall having a plurality of inlet openings and an outlet sealing wall spaced apart axially therefrom and having a plurality of outlet openings, said walls being mounted in a rotatable and sealed manner in the cylindrical pump casing. A suction chamber is arranged in the pump casing upstream of the inlet sealing wall in the delivery direction, and a pressure chamber is arranged downstream of the inlet sealing wall in the delivery direction. The suction chamber in each case extends through the inlet openings into individual suction chamber elements, which reach as far as the outlet sealing wall, while the pressure chamber extends through the outlet openings into individual pressure chamber elements which reach as far as the inlet sealing wall. The suction chamber elements and the pressure chamber elements are in each case arranged in the interspaces between a planet gear, the internal gear and the sun gear and are sealed off from one another by the inlet and the outlet sealing wall and by parts, filling the interspaces, of the solidly designed planet carrier arranged between the inlet and the outlet sealing wall. The feed line for the medium to be delivered runs in the form of a longitudinal bore, which changes into a transverse bore within the axis of rotation of the planet carrier led through the wall of the pump casing, while the discharge line for the delivered medium is guided in a corresponding way through the axis of rotation of the sun gear. Because of the small diameters of the bores and the small cross-sectional areas of the inlet and outlet openings, such a pump would be unsuitable for delivering highly viscous media and would not be self cleaning.

[0004] Another gear pump operating as a planet gear pump is disclosed by U.S. Pat. No. 3,870,437. In this case, the column to be delivered is in each case enclosed in the interspace between the sun gear and the internal gear and two immediately adjacent planet gears. In order to enlarge the size of this interspace continuously in the region of the suction point (inflow region) during the revolution of the planet gears in order to produce the pumping action, and in order to reduce it continuously in the region of the pressure zone (outflow region), this pump has flexibly deformable gears. For example, the internal gear and the driven sun gear can be arranged eccentrically in relation to one another, and flexible planet gears can be used, which are able to adapt to the different gap widths between internal gear and sun gear by deformation (ovality).

[0005] A common feature of these known planet gear pumps is that not only the planet gears but also the internal gear and the sun gear in each case have teeth, which intermesh with one another with the effect of a revolving gear mechanism. When processing plastic melts or rubber mixtures, gear pumps have hitherto been usual, operating with the effect of a spur gear mechanism and generally being connected to a screw extruder. As a rule, the gear pump in this case has a drive which is separate from the drive of the extruder shaft or shafts. Such an extruder is disclosed by EP 0 508 080 A2, for example. In this case, an extruder screw delivers the material to be extruded directly into the pocket area of the gear pump, which has two intermeshing spur gears. This type of gear pump is not self cleaning and therefore, generally when the respective material to be processed is changed, requires complicated dismantling and cleaning work in order not to accept any quality losses following a material change.

[0006] EP 0 564 884 A1 discloses a double screw extruder whose screw shafts in a section to increase the pressure of the melt to be processed are in each case fitted with one of the two spur gears of a gear pump, so that the gears are driven directly by the screw shafts. By means of two sealing walls at the end, that is to say running at right angles to the longitudinal axis of the screw shafts, which are provided with a passage window for the melt to the inlet side and to the outlet side, suction chamber and pressure chamber are divided from each other. This gear pump is not self cleaning either. Its delivery volume cannot be changed independently of the rotational speed of the screw shafts.

[0007] Finally, EP 0 642 913 A1 discloses a single-screw extruder which, before its last screw section, has a gear pump in a spur gear mechanism design. One of the two spur gears of the gear pump is fixed directly to the screw shaft of the screw extruder and is driven by said shaft. The extruder casing has a lateral bulge, in which the second spur gear of the gear pump is mounted. In each case a sealing wall bears on the flat sides of the spur gears, being mounted with a form fit in the casing of the extruder. The sealing walls or the extruder casing are in each case provided with a passage window on the suction side and pressure side for the extruded material. No self cleaning is ensured in this known extruder either.

[0008] It is an object of the invention to propose a screw extruder and gear pump arrangement which, in a particular way, is suitable for processing highly viscous materials and operates largely in a self-cleaning manner.

[0009] This object is achieved by the features of patent claim 1.

[0010] Advantageous developments of this gear pump emerge from the dependent subclaims.

[0011] The present invention provides a screw extruder and gear pump arrangement in which the gear pump is constructed in principle so as to correspond with an epicyclic gearbox and, in a particular way, is suitable for delivering highly viscous media such as plastic melts and rubber mixtures and has the advantage of extensive self cleaning, since the medium to be delivered can be fed in without a significant pilot pressure. The invention is based on a planet gear pump which has a planet carrier which is fitted with at least one planet gear rotatably mounted in the planet carrier. In addition, this planet gear pump has two further functional elements which interact with the at least one planet gear with the effect of a sun gear and an internal gear respectively. Furthermore, a pump casing, which surrounds the planet carrier with the planet gears and the two aforementioned functional elements from the outside, and an inlet and an outlet sealing wall. The inlet sealing wall is firmly fixed to the planet carrier so as to rotate with it and has at least one inlet opening for the medium to be delivered. In a corresponding way, the outlet sealing wall is firmly connected to the planet carrier so as to rotate with it and is provided with at least one outlet opening for the medium to be delivered. In addition, this gear pump has a suction chamber and a pressure chamber, which are enclosed by the pump casing and sealed off from one another, the suction chamber being arranged upstream of the inlet sealing wall in the delivery direction and extending through the at least one inlet opening into at least one suction chamber element along the at least one planet gear as far as the outlet sealing wall, and the pressure chamber being arranged behind the outlet sealing wall in the delivery direction. According to the invention, in a gear pump of this type, provision is made for in each case only one of the two functional elements acting as sun gear or as internal gear to have toothing which meshes with the at least one planet gear, while the other functional element has at least one sealing region which has a smooth wall and is designed in such a way that, over part of the circumference and over the length of the at least one planet gear, it bears on the latter in a sliding and sealing manner. Furthermore, the invention provides for the functional element which has the at least one sealing region to be firmly connected to the planet carrier so as to rotate with it, that is to say executes the same movements. In order to ensure sealed division of the at least one suction chamber element from the at least one pressure chamber element, the invention provides, as a further essential feature, for at least one dividing wall extending from the inlet sealing wall as far as the outlet sealing wall to be arranged, offset in the circumferential direction with respect to the at least one planet gear, said dividing wall being connected to the functional element which has the at least one smooth-wall sealing region in a rotationally fixed and leakproof manner and extending in the radial direction as far as the tip circle of the teeth of the functional element having the teeth.

[0012] In an expedient embodiment, provision is made for the pressure chamber to extend through the at least one outlet opening into at least one pressure chamber element along the at least one planet gear as far as the inlet sealing wall. This means that the pressure chamber element and the suction chamber element in each case lie opposite each other with respect to the planet gear.

[0013] In another embodiment, provision is made for the volume of the respective pressure chamber element to be minimized and preferably to become zero. This means that the dividing wall bears in a leakproof manner on the teeth of the planet gear, in each case over the entire axial length of the respective planet gear and over the entire area of its circumference. In this design, particularly effective self cleaning of the gear pump is ensured.

[0014] The functional element which is toothed in the corresponding way to that of the at least one planet gear and meshes with the latter is preferably the internal gear. Since this can be arranged to be stationary, it is expediently made in one piece with the pump casing or at least mounted in a rotationally fixed manner in the pump casing surrounding the internal gear. In this case, the planet carrier revolves with the functional part corresponding to the sun gear and is preferably formed in one piece with the latter. In this case, there is therefore no toothed sun gear, as in a conventional planet gear mechanism. In this case, the at least one planet gear therefore does not mesh with teeth on such a sun gear either, but moves in a sliding and sealed manner in the at least one sealing region of the functional part otherwise functioning as a sun gear.

[0015] It is of course possible to select a converse arrangement as well, in which a toothed sun gear is used, while the functional part functioning as an internal gear has no teeth but is provided with the at least one sealing region. In this case, the “internal gear” can remain stationary like the planet carrier. Because of the simpler construction, however, the aforementioned solution with a toothed internal gear and with an untoothed “sun gear” is preferred.

[0016] A plurality of planet gears, dividing walls, inlet and outlet openings are expediently provided, that is to say in each case at least two, preferably in each case at least four. The toothing of the planet gears and of the functional part meshing therewith (preferably therefore the internal gear) can have straight teeth, but is preferably designed with oblique teeth. This permits particularly uniform delivery from the planet gear pump according to the invention.

[0017] The planet gears and the functional part meshing therewith can also be designed with herringbone teeth. In this case, however, dismantling is made more difficult. However, by means of a divided design, for example of the internal gear, dismantling may still be provided even under these more difficult conditions.

[0018] In a further expedient embodiment, the invention provides for the dividing walls to run in a spiral shape in the actual direction in a manner corresponding to that of the oblique toothings. In this case, it is recommended to form the dividing walls in one piece with the functional element having the at least one sealing region, that is to say preferably with the “sun gear”. In addition, in this case the planet carrier will expediently be formed in one piece with the “sun gear”.

[0019] The planet gears will expediently be mounted in the inlet sealing wall and the outlet sealing wall, so that these are part of the planet carrier. Of course, a separate formation of these components is also possible. In order that the planet gears can easily be assembled and dismantled, it is advantageous to form only one of the two sealing walls, preferably the inlet sealing wall, in one piece with the planet carrier and to leave the other sealing wall as a separate component.

[0020] In order to be able to accommodate the gear pump easily in the casing of a screw extruder and to ensure that disassembly is simple, it is recommended to configure the outer diameter of the inlet sealing wall to be unequal to, that is to say preferably smaller than the outer diameter of the outlet sealing wall. As a result, the gear pump, which is generally connected to a screw extruder at the delivery end of the latter, can easily be pulled out of the casing at the top end of the extruder.

[0021] In order to permit a change in the delivery volume of the gear pump during operation, a further preferred embodiment of the invention provides for the planet carrier, together with the functional part corresponding to the sun gear and the inlet and the outlet sealing wall, to be arranged in the pump casing such that they can be displaced axially by a displacement travel with respect to the toothed internal gear. As a result, the length of the tooth engagement between the internal gear and the planet gears, and therefore the displacement volume of the teeth, can be varied. In order that no undesired leaks arise between the suction chamber and the pressure chamber, it is recommended that the inlet sealing wall, which is mounted in a sliding and sealing manner in the pump casing and moves into the toothed area of the internal gear when it is displaced, to have an axial thickness (that is to say as viewed in the displacement direction) which is greater than the maximum displacement travel w. As a result, the seal between the pump casing and the inlet sealing wall is maintained unchanged. However, provision can also be made to set a certain leakage between pressure chamber and suction chamber by means of a slight displacement, in order to restrict the delivery capacity of the pump.

[0022] As distinct from known planet gear pumps, restricting the delivery capacity during operation is possible without a continually required second drive for one of the functional elements (internal gear or sun gear), since a drive with a power consumption which is to this extent extremely small is only required for the short time of the axial displacement of the gear pump. As a result of the ability to adjust the delivery capacity of the gear pump, adaptation to the processing of different materials is possible.

[0023] From a production point of view, it may be recommendable for the planet gears and/or the internal gear or sun gear meshing therewith to be of soft elastic design in the region near to the surface of the toothing. In this case, as compared with exact toothing, in production terms relatively coarsely toleranced metallic basic tooth bodies can be produced, which have smaller dimensions than the intended dimensions of the finished toothing and are subsequently provided with an elastic covering, in particular a covering of rubber or a thermoplastic elastomer. Since this covering has excellent elasticity characteristics, the requirements on the toothing produced in this way are also lower than in the case of purely metallic toothing. Oversizes can be compensated for to the same extent by deformation. By means of a rubber covering with a slight oversize, the teeth cavities of the internal gear can be cleaned out completely.

[0024] In a further variant, the invention provides for the toothing of the internal gear or the planet gears to be designed alternately or in sections with teeth of different height, that is to say for example to use a planet gear in which half the teeth have a normal size and the other half of the teeth have a reduced size, the two tooth sizes alternating continuously over the circumference. If the pump has a plurality of planet gears, different planet gears can also be used, that is to say planet gears with a normal tooth height and other planet gears with a reduced tooth height. The effect which can be produced therewith is to be seen in the fact that, as a result of partly reduced tooth height, it is possible to carry out compaction of the material which is contained in the tooth gaps of the opposing gear interacting with the respective gear. Only when it encounters a tooth of full design would the compacted material then be forced out of the tooth gap and delivered.

[0025] In the case of a planet gear with a continuously reduced tooth height, therefore, the material located in the tooth gaps in the internal gear will first of all be compressed and in each case pressed out of the tooth gaps, subjected to expansion and shear flows only by the following planet gear, whose teeth are of full design. In the case of a gear pump having four planet gears, in each case two opposite planet gears are formed with a reduced teeth height and the two other opposite planet gears are formed with a normal tooth height. The positive flows present in the gear pump promote continuous homogenization and mixing (for example fillers) of the material to be processed.

[0026] The tooth geometry of the toothing of planet gears and internal gear is in principle any desired. It is merely necessary to ensure that the teeth of one gear engage in the tooth gaps in the respective other gear in such a way that there is a sealed sliding contact with the two teeth bounding the respective tooth gaps of the other gear.

[0027] According to the invention, one or more gear pumps in the design of an epicyclic gear mechanism, in particular gear pumps, are used in a screw extruder for delivering free-flowing media such as in particular plastic melts and rubber mixtures, it being possible for the screw extruder to have one or else more screw shafts and for the screw shaft or shafts in each case to be coupled mechanically to the drive of the gear pump, so that it does not require a separate pump drive. No dedicated control for the drive of the gear pump is needed either.

[0028] The pump casing is normally connected directly to the casing of the screw extruder or is preferably a constituent part of the extruder casing.

[0029] It is particularly advantageous for the number of turns on the screw shaft or shafts at the delivery end in each case to be chosen to be equal to the number of planet gears of the gear pump connected thereto. However, the number of turns must in no way be constant over the entire screw length. One preferable use of the gear pumps according to the invention provides for the number of turns on the screw shafts in the section of the screw shafts lying upstream of the delivery end in each case to be chosen to be half as great as at the delivery end.

[0030] When a planet gear pump with oblique toothing is used, it is advantageous to provide the inclination of the spiral of the turns of the screw shafts in each case in the opposite direction to the inclination of the toothing, based on the delivery direction of the screw extruder.

[0031] In order to be able to effect the delivery capacity of the screw extruder having the planet gear pump without changing the drive speed, it is recommended to arrange the screw shaft to be displaceable axially, in each case together with the planet carrier and the sun gear and the inlet and outlet sealing wall. As a result of axial displacement of the screw shaft, which is firmly connected mechanically to the planet carrier so as to rotate with it, the delivery capacity of the gear pump can be influenced in this way, since in the manner previously described, the displacement volume and/or the desired leakage between suction chamber and pressure chamber is controlled.

[0032] A substantial advantage in the case of the combination of a screw extruder with the gear pump is to be seen in the fact that, because of the good pressure build-up characteristic with the simultaneous lack of necessity for a noticeable delivery pressure in order to feed into the gear pump, the extruder screw upstream of the gear pump can be of very short design. The length of the extruder screw is preferably two to fifteen times the value of the screw diameter.

[0033] A particularly advantageous use of the planet gear pump results in a screw extruder in particular for processing rubber mixtures if, downstream of the gear pump, there is an extruder pin cylinder region, such as is disclosed for example by DE-40 39 942 A1, whose disclosure content to this extent is incorporated in the present application. In this case, the planet gear pump can easily build up the high pilot pressure which is advantageous for the extruder pin cylinder region.

[0034] In a further advantageous application, provision is made for a vacuum degassing region also to be connected downstream of such an extruder pin cylinder region, being followed at the end of the extruder by a second planet gear pump in order to supply the required extrusion pressure at the extruder outlet.

[0035] In the following text, the invention will be explained in more detail using exemplary embodiments illustrated in the figures in which, in a schematic representation:

[0036]FIG. 1 shows a longitudinal section through a single-screw extruder with planet gear pump,

[0037]FIG. 2 shows the longitudinal section according to FIG. 1 in the form of a development,

[0038]FIGS. 3a-d show cross sections according to the lines A-A, B-B, C-C and D-D in FIG. 1,

[0039]FIG. 4 shows a modification of the screw extruder according to FIG. 1 resulting from axial displaceability of the screw shaft,

[0040]FIG. 5 shows a screw extruder with planet gear pump and extruder pin cylinder region connected thereto,

[0041]FIG. 6 shows a screw extruder with two planet gear pumps connected one behind another, extruder pin cylinder region and vacuum degassing region,

[0042]FIG. 7 shows a sectional image of a planet gear with soft elastic covering and

[0043]FIG. 8 shows a planet gear with teeth of alternately different heights.

[0044] In FIGS. 1 to 3 d, a screw extruder 15 is illustrated in an axial longitudinal section, a number of cross sections and a schematic development (FIG. 2). The screw extruder 15 has a screw shaft 17 which, viewed in the delivery direction, is initially of two-turn design and at the delivery end 19 has twice the number of turns, that is to say has four turns. The screw shaft 17 is surrounded by an extruder casing 16. Immediately following the delivery end 19, a planet gear pump 18 is provided, which has a substantially cylindrical pump casing 4, within which a planet carrier 2 with four planet gears 1 rotatably mounted therein is arranged. Provided in the region of the wall of the pump casing 4, on the inside, is a toothed internal gear 3 which, in a preferred embodiment of the invention, is designed in one piece with this part of the pump casing 4. On the left-hand side of the planet gears 1 there is an inlet sealing wall 5, which is mounted in a sealed and rotatable manner in the extruder casing 16. This inlet sealing wall 5 is provided with four inlet openings 6, corresponding to the number of planet gears 1 (FIG. 3a). Arranged on the right-hand side of the planet gears 1 is an outlet sealing wall 7, which is provided in a corresponding way with four outlet openings 8 (FIG. 3d). The outlet sealing wall 7 is also rotatably mounted, to be specific in the pump casing 4. To the left of the inlet sealing wall 5, that is to say at the end of the four-turn part of the screw shaft 17, there is the suction chamber 9 of the gear pump 18, while its pressure chamber 10 is located on the right-hand side of the outlet sealing wall 7. The suction chamber 9 extends through the inlet openings 6 in the form of suction chamber elements 9 a in each case along a planet gear 1 as far as the outlet sealing wall 7. In a corresponding way, in each case on the diametrically opposite side of a planet gear 1, the pressure chamber 10 extends in the form of a pressure chamber element 10 a in each case through the outlet openings 6 as far as the inlet sealing wall 5 (FIGS. 1, 3b, 3 c). The planet carrier 2, to which in functional terms the inlet sealing wall 5 and the outlet sealing wall 7 also belong, since these accommodate the mounting of the planet gears 1, is provided with a total of four dividing walls 12, which extend substantially radially from a central basic body outward between the planet gears 1 as far as the toothing of the internal gear 3. FIG. 3b reveals that the planet gears 1, in each case in a sealing region 11 of smooth cylindrical shape, bear in a sliding and sealing manner on the respectively associated dividing walls 12 and the central basic body of the planet carrier 2. The sealing walls' 12 are designed in one piece with the planet carrier 2. The planet gears 1 are engaged with the toothing of the internal gear 3, so that sealed contact is also provided there. Viewed in cross section, therefore, the suction chamber elements 9 a are in each case terminated by a dividing wall 12, the central basic body of the planet carrier 2, an associated planet gear 1, which bears in a sealing manner on the central basic body and the toothing of the internal gear 3, and by part of the internal gear 3. This applies in a corresponding way for the pressure chamber elements 10 a which in each case lie diametrically opposite the axis of the planet gears 1 and, in the illustrated sectional position of FIG. 3b, have only a very small cross section in the vicinity of the inlet sealing wall 5. The converse size relationships result in the case of a corresponding section in the vicinity of the outlet sealing wall 7. There, the suction chamber elements 9 a would have the size of the pressure chamber elements 10 a in FIG. 3b. The cross section of the pressure chamber element 10 a would accordingly in each case have the size of the suction chamber element 9 a in FIG. 3b. This therefore means that the suction chamber elements 9 a decrease continually in cross section from the inlet opening 6 as far as the outlet sealing wall 7, while the opposite pressure chamber elements 10 a increase continuously in cross section from the inlet sealing wall 5 as far as the outlet openings 8 in the outlet sealing wall 7. In the center between the inlet sealing wall 5 and the outlet sealing wall 7, the suction chamber elements 9 a, as FIG. 3c shows, have a cross section of about the same size as the pressure chamber elements 10 a.

[0045] The volume of the pressure chamber elements 10 a could also be reduced down to zero as required in order to increase the self-cleaning capability of the planet gear pump 18, so that the dividing walls 12 would in each case bear in a sealing manner on the toothing of the respective planet gears 1, on the side lying opposite the suction chamber elements 9 a, and the material to be delivered would pass directly from the tooth gaps of the toothing of the planet gears 1 and of the internal gear 3 through the outlet openings 8 into the pressure chamber 10.

[0046] While the central basic body of the planet carrier 2 which, in a conventional planet gear mechanism corresponds to the sun gear, has no toothing of any kind, the internal gear 3 is advantageously equipped with oblique toothing, just like the planet gears 1. Likewise, in a preferred development of the invention, the dividing walls 12 are spiral shaped, that is to say set obliquely with respect to the longitudinal axis of the screw extruder 15, the inclination of this obliqueness pointing in the opposite direction to the inclination of the turns of the screw shaft 17 (FIG. 1). The outlet from the extruder illustrated is designated by the reference symbol 22.

[0047] The section of FIG. 1 reveals that the pump casing 4 has an enlarged diameter as compared with the extruder casing 16. The extruder casing 16 has an inner diameter which is slightly smaller than the diameter of the tip circle of the toothing of the internal gear 3, so that the right-hand end wall of the extruder casing 16 in the vicinity of the section B-B shown completely covers the cross-sectional areas of the tooth gaps of the toothing of the internal gear 3. The same applies to the tooth gaps of the planet gears 1 if the latter are located in the region of engagement with the toothing of the internal gear 3. Otherwise, the planet gears 1 and the entire intermediate space are closed completely by the inlet sealing wall 5, apart from the necessary inlet openings 6 (FIG. 3a). The same is true on the other side of the planet gears 1 in relation to the outlet sealing wall 7 and the outlet openings 8 (FIG. 3d). The outlet sealing wall 7 has an outer diameter which corresponds to the inner diameter of the pump casing 4, so that the tooth gaps of the toothing of the internal gear 3 on the right-hand end of the toothing are sealed completely by the outlet sealing wall 7. Since the outer diameter of the inlet sealing wall 5 is deliberately chosen to be smaller than the tip circle diameter of the toothing of the internal gear 3, for the purpose of disassembly, after a top piece 25 has been removed, the entire unit of the planet carrier 2 with the planet gears 1 and the two sealing walls 5, 7 can be pulled to the right out of the pump casing 4 without difficulty.

[0048] The mode of operation of the screw extruder illustrated is as follows: the medium to be processed, for example the melt of a thermoplastic, is delivered from left to right in the direction of the gear pump 18 by the screw shaft 17. From the initially two part streams which move along the two-turn screw shaft, four part streams are produced at the delivery end 19 by the two additional screw turns. The screw turns in each case end, as emerges particularly clearly from the development of FIG. 2, as an inlet opening 6, that is to say open into a suction chamber element 9 a. Since the screw shaft 17 is coupled mechanically to the planet carrier 2, the latter, together with the sealing walls 5, 7 likewise coupled thereto, carries out the same rotational movements. The melt passes through the comparatively large inlet openings 6 into the individual suction chamber elements 9 a, without a substantial pilot pressure being needed for this purpose. The material of the melt is swept through the dividing walls 12 into the tooth gaps in the toothing of the internal gear 3 in accordance with the direction of rotation shown. The conveyance of the melt into the respective opposite pressure chamber element 10 a takes place in two part streams at each planet gear 1. One part stream is guided in the tooth gaps of the respective planet gear 1 along the sealing zones 11 into the associated pressure chamber element 10 a, while a second mass flow is produced by the melt being squeezed out of the tooth gaps of the internal gear 3 because of the engagement of the toothing of the planet gears 1. In this way, the overall stream still consisting of four part streams is then divided up into a total of eight part streams, so that the planet gear pump can contribute to improving the mixing of the material. The fact that the material to be delivered is swept into the tooth gaps of the internal gear 3 by the radial dividing walls 12 as the planet carrier 2 revolves also results in this gear pump being particularly suitable for extensive self cleaning.

[0049] The inlet sealing wall 5 and therefore at least also part of the planet carrier 2 can also be a bodily constituent part of the screw shaft 17, that is to say do not have to be separate components.

[0050]FIG. 4 illustrates a modification of the screw extruder with planet gear pump illustrated in FIGS. 1 to 3 d. The fundamental construction and function of this screw extruder correspond to the last one, so that to this extent reference is made to the above description. However, as distinct from this, the screw shaft 17 of the screw extruder 15 in FIG. 4 can be displaced in the axial direction, together with the planet carrier 2 and the inlet sealing wall 5 and outlet sealing wall 7 connected thereto, as indicated by the thick double arrow shown on the longitudinal axis of the extruder. The tooth width of the internal gear 3 is designated b₁ and the tooth width of the planet gears 1 is designated b₂. The two tooth widths b₁, b₂ are approximately equal, so that in an initial position (not shown), in which the screw shaft with the planet carrier 3 coupled mechanically thereto is displaced to the left (left-hand end position) both toothing widths b₁, b₂ are completely covered. The displacement travel of the screw shaft 17 and of the planet carrier 2, which has occurred with respect to this initial position, is designated by w in FIG. 4. Thus, in the position shown (in the vicinity of the right-hand end position), the toothing is engaged only over a length b₁−w. The delivery volume of the gear pump 18 is accordingly reduced. In this case, the part stream of the delivered quantity led past the sealing regions 11 (FIGS. 3b, c) remains completely unaffected. The only part stream which is changed is the part mass stream caused by the displacement of the teeth of the planet gears 1 engaging in the tooth gaps of the internal gear 3. In order to prevent the axial displacement of the planet carrier 3 of the gear pump 18 causing an undesired leakage between the pressure chamber 10 and the suction chamber 9 in the region of the tooth gaps on the left-hand side of the internal gear 3, the thickness of the inlet sealing wall 5, which is designated d, is considerably greater than the thickness of the outlet sealing wall 7. In order to obtain the tightness, this thickness d must be at least slightly greater than the maximum displacement travel w, in order that the circumference of the inlet sealing wall 5, in spite of the displacement, continues to bear tightly on the smooth-walled inside of the extruder casing 16 or of a pump casing 4 extended in this region. If this overlap of the inlet sealing wall 5 with the extruder casing 16 were not provided, a reverse flow from the pressure chamber 10 would be produced through those tooth gaps in the internal gear 3 which are currently not in engagement with the corresponding teeth of the planet gears 2. This reverse flow effect could, however, also be produced and controlled deliberately in order to regulate the delivery capacity of the pump. To this extent, the considerable enlargement of the thickness of the inlet sealing wall 5 is not absolutely necessary in order to maintain the functional capability of the gear pump 18 in spite of the displacement of the planet carrier 3 in the axial direction. In this way, the delivery capacity of the gear pump 18 can even be reduced much more substantially than is possible in the embodiment illustrated in FIG. 4.

[0051]FIG. 5 shows a similar arrangement of screw extruder 15 with gear pump 18, which is supplemented only by the feature that, in the delivery direction, which goes from left to right, an extruder pin cylinder region 20 is also connected downstream of the gear pump 18, such as is often used in particular for processing rubber mixtures. Pins 23 are inserted into the housing of the extruder pin cylinder region 20, as indicated by the double arrows, and can be set in the radial direction against the extruder longitudinal axis. In this case, the gear pump 18 ensures that there is still sufficient pressure for the extrusion of the processed material at the end of the extruder pin cylinder region 20.

[0052] In FIG. 6, the arrangement according to FIG. 5 is further extended by two further sections. To be specific, the extruder pin cylinder region 20 is firstly adjoined in the delivery direction by a vacuum degassing region 21 having a vacuum connection 24 and a blister 26 on the inlet side, and also by a four-turn screw shaft 17, while at the extrusion end, that is to say at the right-hand end of the arrangement, a second gear pump 18 is also connected, which produces the delivery pressure desired for extrusion of the processed melt. In this arrangement, by means of volumetric delivery through the two gear pumps 18, decoupling of the build-up length and extrusion pressure is made possible, so that flooding of the vacuum extraction in the vacuum degassing region 21 can be avoided.

[0053] For the toothing of the internal gear 3 (or the toothing of the sun gear in the case of a converse pump arrangement) and/or the toothing of the planet gears 1, it is possible to select an embodiment as illustrated in FIG. 7 as an example and schematically as a part section of a planet gear 1. This planet gear 1 has a basic gear body 13 which is preferably produced from metal (for example steel) and in production terms can be toleranced relatively coarsely in relation to the toothing. The individual teeth are substantially smaller and the tooth gaps are substantially larger than is intended for the final shape of the planet gear 1. This final shape is produced by a covering of a soft elastic material 14 (for example rubber or a thermoplastic elastomer). Because of the good deformability of this material, the accuracy of shape of the finished planet gear 1 does not have to be so high as would have to be the case with a rigid material, since oversizes of the tooth geometry can be compensated for by deformation during the tooth engagement. Because of the lower requirements on the accuracy of shape, the production expenditure for the toothing can be reduced accordingly. On the other hand, in this way particularly high requirements on the tightness of the toothing which is in engagement with regard to an undesired reverse flow of material can also be met.

[0054] In FIG. 8, a further variation with regard to the toothing that can be used is again indicated schematically using the example of a planet gear 1, which is illustrated as a detail. This planet gear 1 has teeth with alternately different heights. The difference in the teeth height is designated by Δh. In this case, each second tooth has a lower tooth height than the normal tooth height. Alternatively, a plurality of teeth one after another could in each case have the same height, so that the tooth height would change in areas over the circumference. It is also possible to use planet gears 1 which intrinsically in each case have the same tooth height but mutually different tooth heights.

[0055] A particular effect could be achieved with this, namely compaction of the material in a tooth gap in the internal gear 3, which is acted on by a tooth with a reduced tooth height and, as a result, is at most conveyed partly out of the tooth gap into the pressure chamber 10. As a result of another tooth with a normal tooth height penetrating into such a tooth gap during the further revolution of the planet carrier, this compacted material could then be delivered into the pressure chamber.

[0056] The design proposed by the invention for a gear pump ensures that during empty running of an extruder equipped with such a gear pump, virtually the entire melt material is delivered out of the extruder and the gear pump connected thereto, since virtually no pilot pressure is required to ensure the feed of material into the gear pump. In this way, in most cases complicated cleaning work when changing the material to be processed may be avoided. Added to this is the fact that, because of the division of the material flows at each planet gear into two smaller part flows, this gear pump has a considerably better mixing action on the material to be processed than is the case in a conventional gear pump used as a melt pump and having the design of a spur gear mechanism. There, only two material part streams are produced and led together again. In the gear pumps illustrated in the figures, which are each equipped with four planet gears, eight part streams are produced in the melt flow and led together again. As a result, significantly better material mixing is ensured. By means of simple mechanical coupling of the planet carrier to the screw shaft of an extruder, it is possible to dispense completely with a separate motor drive for the gear pump. Nevertheless, regulation of the delivery capacity of the gear pump is possible if the latter is set up for axial adjustment, as has been described above.

[0057] List of Reference Symbols

[0058]1 Planet gear

[0059]2 Planet carrier

[0060]3 Internal gear

[0061]4 Pump casing

[0062]5 Inlet sealing wall

[0063]6 Inlet opening

[0064]7 Outlet sealing wall

[0065]8 Outlet opening

[0066]9 Suction chamber

[0067]9 a Suction chamber element

[0068]10 Pressure chamber

[0069]10 a Pressure chamber element

[0070]11 Sealing region

[0071]12 Dividing wall

[0072]13 Basic gear body

[0073]14 Soft elastic covering

[0074]15 Screw extruder

[0075]16 Extruder casing

[0076]17 Screw shaft

[0077]18 Gear pump

[0078]19 Delivery end

[0079]20 Extruder pin cylinder region

[0080]21 Vacuum degassing region

[0081]22 Extruder outlet

[0082]23 Adjustable pin

[0083]24 Vacuum connection

[0084]25 Top piece

[0085]26 Blister

[0086] b₁ Internal gear tooth width

[0087] b₂ Planet gear tooth width

[0088] w Displacement travel

[0089] d Thickness of inlet sealing wall

[0090] Δh Difference in the tooth heights 

Patent claims
 1. A screw extruder and gear pump arrangement for highly viscous media, in particular for plastic melts and rubber mixtures, having one or more screw shafts (17) and a gear pump (18) which in drive terms is coupled mechanically to the screw shaft or shafts and whose pump casing (4) is a constituent part of the casing (16) of the screw extruder (15) or is connected directly thereto, having a planet carrier (2) fitted with at least one rotatably mounted planet gear (1), having two further functional elements, which interact with the at least one planet gear (1) with the effect of a sun gear or an internal gear (3), having a pump casing (4) surrounding the planet carrier (2), having an inlet sealing wall (5), which is firmly connected to the planet carrier (2) so as to rotate with it and has at least one inlet opening (6) for the medium to be delivered, having an outlet sealing wall (7), which is firmly connected to the planet carrier (2) so as to rotate with it and has at least one outlet opening (8) for the medium to be delivered, and having a suction chamber (9) and a pressure chamber (10), which are enclosed by the pump housing (4) and sealed off from one another, the suction chamber (9) being arranged upstream of the inlet sealing wall (5) in the delivery direction, extending through the at least one inlet opening (6) into at least one suction chamber element (9 a) along the at least one planet gear (1) as far as the outlet sealing wall (7), and the pressure chamber (10) being arranged behind the outlet sealing wall (7) in the delivery direction, in each case only one of the two functional elements acting as sun gear or internal gear (3) having teeth meshing with the at least one planet gear (1), and the other functional element having at least one sealing region (11), which is designed to be smooth-walled and to bear in a sliding and sealing manner over part of the circumference and over the length of the at least one planet gear (1), the other functional element, having the at least one sealing region (11) being firmly connected to the planet carrier (2) so as to rotate with it, and in that in order to separate the at least one suction chamber element (9) from the at least one pressure chamber element (10 a), at least one dividing wall (12) extending from the inlet sealing wall (5) as far as the outlet sealing wall (7) is arranged to be offset in relation to the at least one planet gear (1) in the circumferential direction, being firmly connected in a sealing manner to the other functional element having the at least one smooth-walled sealing region (11), so as to rotate with it, and extending in the radial direction as far as the tip circle of the toothing of the functional element having the toothing.
 2. The screw extruder and gear pump arrangement as claimed in claim 1, characterized in that the pressure chamber (10) extends through the at least one outlet opening (8) into at least one pressure chamber element (10 a) along the at least one planet gear (1) as far as the inlet sealing wall (5).
 3. The screw extruder and gear pump arrangement as claimed in claim 1, characterized in that the at least one dividing wall (12) bears on the toothing of the planet gear (1), over the entire area of its circumference, in each case over the entire axial length of the at least one planet gear (1).
 4. The screw extruder and gear pump arrangement as claimed in one of claims 1 to 3, characterized in that in each case at least two, in particular in each case at least four, planet gears (1), dividing walls (12) inlet (6) and outlet openings (8) are provided.
 5. The screw extruder and gear pump arrangement as claimed in one of claims 1 to 4, characterized in that the toothing of the at least one planet gear (1) and of the toothed functional element is designed as oblique toothing.
 6. The screw extruder and gear pump arrangement as claimed in claim 5, characterized in that the at least one dividing wall (12) runs spirally in the axial direction in accordance with the oblique toothing.
 7. The screw extruder and gear pump arrangement as claimed in one of claims 1 to 6, characterized in that the at least one dividing wall (12) is formed in one piece with the functional element having the at least one sealing region (11).
 8. The screw extruder and gear pump arrangement as claimed in one of claims 1 to 7, characterized in that the internal gear (3) having the toothing and the functional part corresponding to the sun gear is provided with the at least one sealing region (11).
 9. The screw extruder and gear pump arrangement as claimed in claim 8, characterized in that the planet gear (2) and the functional part corresponding to the sun gear are formed in one piece.
 10. The screw extruder and gear pump arrangement as claimed in claim 8 or 9, characterized in that the inlet sealing wall (5) or the outlet sealing wall (7) is formed in one piece with the planet carrier (2).
 11. The screw extruder and gear pump arrangement as claimed in one of claims 8 to 10, characterized in that the internal gear (3) is formed in one piece with that part of the pump casing (4) which surrounds the internal gear (3).
 12. The screw extruder and gear pump arrangement as claimed in one of claims 8 to 11, characterized in that the outer diameter of the inlet sealing wall (5) is unequal to, in particular smaller than, the outer diameter of the outlet sealing wall (7).
 13. The screw extruder and gear pump arrangement as claimed in one of claims 8 to 12, characterized in that in order to be able to change the delivery volume of the gear pump (18), the planet carrier (2) together with the functional part corresponding to the sun gear, and the inlet (5) and the outlet sealing wall (7) are arranged within the pump casing (4) such that they can be displaced axially by a displacement travel w with respect to the internal gear (3).
 14. The screw extruder and gear pump arrangement as claimed in claim 13, characterized in that the thickness d (viewed in the displacement direction) of the inlet sealing wall (5) is greater than the maximum displacement travel w.
 15. The screw extruder and gear pump arrangement as claimed in one of claims 1 to 14, characterized in that the at least one planet gear (1) and/or the functional part having the toothing meshing with the at least one planet gear (1) is/are of soft elastic design, at least in the region close to the surface of its toothing.
 16. The screw extruder and gear pump arrangement as claimed in claim 15, characterized in that the toothing is in each case formed by a metallic basic gear body (13) which is coarsely toleranced in production terms and has an elastic covering (14), in particular a covering of rubber or a thermoplastic elastomer, in the toothing region.
 17. The screw extruder and gear pump arrangement as claimed in one of claims 1 to 16, characterized in that the toothing of the internal gear (3) or of the at least one planet gear (1) is designed with teeth of different height alternately or in sections or, in the case of a plurality of planet gears (1), the teeth of at least one of these planet gears (1) have a different tooth height than another planet gear.
 18. The screw extruder and gear pump arrangement as claimed in one of claims 1-17, characterized in that the number of turns at the delivery end (19) of the screw shaft/shafts (17) is in each case equal to the number of planet gears (1) of the gear pump (18) connected thereto.
 19. The screw extruder and gear pump arrangement as claimed in claim 18, characterized in that the number of turns of that section of the screw shaft (17) which lies upstream of the delivery end (19) is in each case half as great as the number of turns at the delivery end (19).
 20. The screw extruder and gear pump arrangement as claimed in one of claims 1 to 19, characterized in that the toothing in the gear pump (18) is of oblique/toothed design and the inclination of the spiral of the turns of the screw shaft (17)—based on the delivery direction of the screw extruder (15)—is in each case opposite.
 21. The screw extruder and gear pump arrangement as claimed in one of claims 1 to 20, characterized in that the screw shaft (17) is arranged to be axially displaceable, in each case together with the planet carrier (2) and the functional part corresponding to the internal gear and also the inlet and the outlet sealing wall (5, 7).
 22. The screw extruder and gear pump arrangement as claimed in one of claims 1 to 21, characterized in that an extruder pin cylinder region (20) is arranged downstream of the gear pump (18) in the delivery direction.
 23. The screw extruder and gear pump arrangement as claimed in claim 22, characterized in that two gear pumps (18) are arranged axially one behind another on one screw shaft (17), the second gear pump (18) in the delivery direction being arranged directly downstream of a vacuum degassing region (21) which adjoins the extruder pin cylinder region (20). 